Method and apparatus for filtering



Nov. 27, 1951 A. O. FINK ETAI- METHOD AND APPARATUS FOR FILTERING 5 sheets-sheet 1 Filed Deo. 3 0, 1947 Invsnron Ahinv D. Fm Dmn E. Blum ArvoRNsvs awww/zw y ril 21731,:

Nov. 27, 1951 A. O. FINK I'AL METHOD AND APPARATUS FOR FILTERING 5 sheets-sheet 2 Filed De'c. 30, 1947 Irwin-rola Ausw 0. Fm {Dnvlo E. Einen Nov. 27, 1951" A. o. FlNK Erm. 2,576,288

METHOD AND APPARATUS FOR FILTJRINGv Filed Dec. 30, 1947 5 ShleetS-Sheei'l 3 INvr-:Nron ALBERT O. Flam Dawm E. BENCH Avonwevs Nov. 27, 1951 A. o. PINK ETAL 2,576,288

METHOD AND APPARATUS FOR FILTERING Filed Dec. 30, 1947 5 SheetsSheet 4 INVENTun Awam- O. Fmn Dunn E, BENCH Bv v JW 5.7m

ATTORNEYS' Nov. 27, 1951 A. o. FINK l-:l-AI.A METHOD AND APPARATUS FOR FILTERING 5 sheets-sheet'- 5 Filed Dec. 30, 1947 ALBERT O. Flu Damp E. Blum A'r-ronuevs Patented Nov. 27, 1951 METHOD AND APPARATUS FOR FILTERING Albert O. Fink and David E. Bench, Dayton, Ohio,

assignors, by mesne assignments, to The Commonwealth Engineeringl Company 'of Ohio, Dayton, Ohio, a corporation of Ohio Application December 30, 1947, Serial No. 794,634

This invention relates to filters, and particularly to automatically operable Vacuum filters, and to methods for carrying out automatic filtering cycles under vacuum.

Most filtering operations are essentially batch type processes. This means that a Vfiltering cycle is carried out for a certain length of time and then is discontinued while readjustments are made in the filtering device. Such readjustments generally consist of washing, removing, or renewing the filtering surface of the filtering member. During this washing, replacingy or renewing operation the filtering device is either idle or has placed therein another filtering member in clean condition.

Certain attempts have been made, especially in connection with vacuum filters, to provide for a continuously operating device by associating with the filtering device the filtering surface renovating or renewing mechanisms.

Such attempts generally took the form of placing within the filtering device a station wherein the filter cake was washed or otherwise treated. Since an operation of this nature on the filtering cake was necessarily completely disassociated from the ltering operation, generally taking place in the atmosphere, this required that la certain portion of the filtering member be blocked off. This was generally accomplished by utilizing internal Valvermeans to isolate that portion of the cake or surface of the filtering member being treated from the remainder thereof and having flow pasages for wash water or air.

By carrying out the caketreatment in the atmosphere a considerable part of the filtering surface of the device is idle, and there is also introduced the possibility of leakage, contamination, cake cracking or dislodging, or, in the case of a non-packing cake, complete disintegration thereof. l

Most filtering operations arel best carried out in connection with a filtering member whose action is augmented by the use of cake forming materials which are generally entitled lter aids.

Filter aids are generally solid substances `in finely divided form which deposit over the filtering member and form a cake which is finely porous and which is effective to remove the substance from the fluid being filtered which it is desired to retain on the filter cake.

It will be obvious that `the nature of the substance being employed as a filter aid will depend on the nature of the fluid being filtered and the substance to be removed therefrom.

While some filter aid substances will form a hard cake on a filtering member the best filter aids will form a cake which is solid and as dense as thefiltering operation requires but which, at the same time, does not form a hard cake in which .the particles ladhere toi one another. f v f 22 Claims. (Cl. 2111-201) While this is the preferred form of filtering cake it introduces the problem of supporting the cake onr the filtering member when there is no iiuid flow through the cake tending to support it against the filtering member support.

In the present type filtering devices it is necessary either to employ a cake forming filter aid which will be self-supporting, in which case the benefits of the preferred type cake are lost, or to permit the cake to fall from the filtering member each time the filter is shut down.

The primary object of the present invention is to provide a method and apparatus for filtering which overcomes'all of the aforementioned objections toprior art filters.

A still further object of this invention is the provision of a filtering device which is fully automatic in operation and which utilizes to the greatest extent'the filtering capacity of the filter member.

A still further object of this invention is to provide an automatic filter which is idle during the periods thatl the fiow rate through the filter is above av predetermined amount.

A still further object of the present invention is to provide a method and apparatus for filtering through a filter cake so arranged that the cake is continuously renovated thereby producing a continuous filter action. y

It is also an object of this invention to provide a method and .apparatus for Aautomatic filtering in which the residue which accumulates on the filter cake is continuously removed and permitted to drain and is then discharged from the filtering device.

A still further object is the provision of a .vacuum type filter having a cake formed thereon of filter aid material and in which the said cake is prevented from dropping from the filter drum when the filter is shut down and there is a loss of `vacuum withinthe said drum.

It is another object of this invention to pro- `vide a drum type vacuum filter wherein the vacuum within the drum assists in recoating the said drum with the proper thickness of filter cake after the residue from the periphery of the drum has been removed.

These and other objects and advantages will become more apparent upon reference to the following description taken in connection with the accompanying drawings in which:

Figure 1 is a vertical 4section taken through a filtering device according to this invention and in connectionY with a tank containing fluid which is to be filtered;

Figure 2 is a plan view of the dervice shown in Figure 1;

Figure 3 is a vertical section indicated by the line 3--3 on Figure l;

Figure 4 is a plan view indicated by the line 4 4 on Figure 1;

Figure 8 is a fragmentary view showing hcwV the cake applied to the filter drum can be reg# ulated in thickness; Y n I Figure 9 is a diagrammatic view showing the lter in section and showing the control syste'rn associated therewith forceffecting full automatic operation of theV device;

Figure 1=0 lis a fragmentary view showing one manner of supporting the cake 'on the filter drum during the time' thev filter is idle;

Figure 11 shows still another arrangement wherein the filter Ycake is continuously" supported;

Figure 12 is a fragmentary view showing another form Lof scraper `blade for use at the leading edge of the reco'ating chamber; and

Figure 13 is 'a sectional view showing the arrangement of the vinternal shield or mask employed in Figure F12.

Referring to the drawings, there is shown therein the filter of the .present invention in connection with 'a processing tank containing duid which Iis to be 'altered This' processing tank may includeY any' of sev= 'eral work' operations such as relec-troprating cycle and is merely for the purpose of ydemonstrating that 'this invention is adapted for use incorincton witha work cycle V'of that nature.

In the the processing tank .is indicated at l and it @unifi-initiates by means of fan aperture 112 the bottom thereof with-ian adjacent tank 14 Tis a 'part of 4the filter proper.

The 'filter `pauper according to this invention includes a drum F6 "which 'is completely submerged iifithin the liquid wi-tien tip-ie at the normali liquid level. This is indicated by the 'liquid level represented by the line T8.

The-drum "i 6 isv rtatablysu 'cr'ted in a "frame work '2e and is adapted for being driven in -rotation by a motor22 which is connected with the 'said drum through the 'gearing -24.

As will be seen 'in Figures 1 and 2 'there is connected with the drum a conduit Y6 which leads tor `'a pump 28 that driven bythe' motor T30.

by a conduit 32 'with the compartment@ at the right end of the processing 'tank 1l). The compartment 34 is formed by a wall `35 which ek- 'tends above the normal liquid level 'of the tank structed is better lshown. in vFigure v-6 wherein it will be Aseen that the drum comprises a vhollow 'center' shaft '4Q which fincludes "the radial bores 42 by means of which the hollow interior of the shaft communicates with the :interior of the drum.

'The drum -includes the :head members vor end plates 4Q mounted on the shaft 40 and rbetween entend the cylindrical supporting member 46. The member 46 is perforated with a "The 'discharge :side 'of lthe pump '28l is connected plurality of holes whereby fluid ow can take place to the interior of the' drum..

Passing around the supporting member 48 is a cloth or screen 43 which is for the purpose of providing direct support for the filter cake deposited on the drum.' It will be understood that the size and number of perforations in the member AH5 and the mesh and material of the cover '48 will be determined by the nature of the lter- 'ing process' which is to be carried out.

The end of the shaft 40 at the end of the drum opposite the gearing 24 terminates in a stu-b part'which telescopes with a hollow member 5) which is connected with the conduit 26. Suitable sealing means such as the resilient annular ring 52 effect a seal between the shaft 4i) and the' member 5G to permit a high vacuum to be drawn within the drum. 4

Due to the fact that the drum is submerged within'the liquid tank lli it is'unnecessary to provide the interior of the drum with. any valving and the entire drum surface is thus subjected to the action of the vacuum therein.

This invention contemplates continuous renewal of the filter cake on the drum. To this end, when the drum rotates the residue accumulated on the surf-ace Vof the cake and a certain portion of the cake are removed therefrom. Immediately following this action a new supply of lter aidl is supplied to the surface of the drum so that the cake can be restored to its original thickness. As mentioned before, the material employed for building up the cake on the drum can comprise-any of yseveral substances, such as carbon, sand, .gels of various types, or any of the several diatomaceous earths The removal of the residue from the surface of the drum is accomplished `by a vscraping knife 54 which is positioned to -bear lagainst the surface of the cake on the drum adjacent lthe -top thereof. The knife 54 is .la portion of an inclined table A'56 which extends upwardly out of the liquid of the tank I4 and over the edge of the said tank. The table is preferably `supported on the edge of the Itank -by means of lbrackets or the like. The residue vand lter cake which are removed Yfrom the drum are `thus forced on to the table 56, from whence they are removed over the edge of the tank and discharged into any suitable container.

The inclined table 56 actssas a 'drain board and :permits substantially all of the filtrate to 'drainpfrom the `residue and cake before it is nally discharged permanently.

Circumferentially `spaced from the scraper blade 54 is a second scraper blade 58. The blade 58 is -at a-greater radial distance from the center of the drum than is the blade 54 and is 'adjusted so that the drum in leaving the Vblade 58 will have exactly `the proper thickness of cake thereon. The blade 58 is preferably supported on the chamber 'B2 'and may lbe made adjustable as shown in Figure 8.

For supplying new Vca-ke tothe 'surface of the drum between the blades 54 and 58, the said blades are connected with end Iplates Si) which bear against the surface of the cakeon the drum at the ends of the blades 54 land 58. These end plates may be rigidly supported in any suitable manner vrelative'to the drum such as by being integral with the 'tank62 asfseenin Figure 4. The end Vplates together with `the `blades 54 and 58 define a recoating chamber which opens directly 'against the surface kof the drum. `A recoating slurry of the proper concentration supplied to this chamber will be operative to rebuild the coat on the drum due to the action of the vacuum Within the drum. This is due to the fact that the said vacuum will draw the liquid from the slurry Vliquid level in the tanks I0 and I4.

For supplying fluid to the tank 62 there is a conduit 64 which leads to the compartment 34 at the end of the processing tank I0. Due to the fact that the liquid level in the compartment 34 is above that in the tanks I0 and I4, the liquid level in the tank 62 will also be substantially above that in the tanks I0 and I4. The purpose of this will become more apparent hereinafter and is to insure a greater pressure within the recoating chamber than is standing on the fluid outside the chamber, thereby preventing the entrance of contaminated fluid to be ltered in the tank I4 into the chamber and contamination of the recoating slurry.

Inasmuch as the slurry in the tank 62 and the recoating chamber consists of a suspension of solid material in a liquid, it is preferable that the slurry be agitated in order to maintain a uniform suspension and to prevent the filtrate from precipitating to the bottom of the slurry tank. Accordingly, there is mounted within the tank 62 a propeller or any other suitable type of agitator 66 which is mounted on a shaft 68 leading to a drive motor l0. The recoating chamber communicates with the tank 62 at somewhat above the center thereof and, as will be seen in Figure 4, is so arranged that the propeller 66 will cause the uid to circulate through the recoating chamber and back to the tank 62. This is accomplished by extending the lower scraper blade 58 horizontally across the tank 62 as at 'I2 and erecting the vertical partition'14 which is cut off at an angle in order to define the triangular passage 'I6 best seen in Figure 4. v

Then, extending horizontally from the top of the partition I4 is a horizontal partition or baffle member 18 which extends over to beneath the right end of the inclined table 56 as seen in Figure 3. The bafe 18 is brought to a position fairly close to both the table 56 and the surface of the drum within the recoating chamber. This brings about this passage of iluid through the recoating chamber as indicated by the arrows in Figure 3 and prevents any accumulation of precipitated filter aid within the chamber. A uniform suspension throughout the tank 62 and recoating chamber is thus maintained at all times.

'For supplying the solid material to the chamber '62 there is provided some suitable form of solid feeding device such as the hopper Bil which is mounted above the tank 62 and which is operable to discharge material thereto upon rotation of the shaft 82 within the hopper by the motor 84.

Rotation of the shaft 82 is effective to discharge material from the hopper by means of the member 86 carried on the shaft 82 and which forces the filter aid material 88 through the screen 90 in the bottom of the hopper.

The principle of operation of the device shown in the drawings is like that of a flour sifter wherein the filter aid material will pass through fthe screen as long as the member 86 rotates but will be supported by the screen whenever the said member ceases to rotate. It will be understood, however, that any of several other devices could be employed for bringing about the feeding of the solid material to the tank 62. The essential feature in connection with the filter aid feeding device is that the discharge of material to the slurry tank be controlled.

Returning to the discharge of the residue and the filter cake removed from the drum by the leading scraper blade 54, the device for moving the substance up the inclined drain board 56 comprises a ladder like device having a plurality of transverse members 92 interconnected by the longitudinal member 94. The end of the member 94 at the discharge end of the table 56 is pivoted to a rod 96 which extends across the top of the tank I4' and is slidably supported in an upstanding bracket 98. Intermediate the ends of the member 94 is a bracket |00 to which is pivoted an arm |02 that extends backwardly to the shaft |04 with which it is connected by the crank member |06. The end of the member 94 adjacent the blade 54 has an upstanding part |08 between which and the arm |02 there bears a spring IIO. With the arm I02 in the position shown the lower end of the member 94 is lowered to bring the transverse parts 92 against the table 56. However, when the shaft |04 and the crank |06 rotate to raise the arm I02, the spring IIIJ and projecting part |08 lift the lower end of the member 94 and raise the transverse parts 92 from the table. In order .to raise the upper end of the member 94 there is an abutment |I2 carried on the arm I02 and which engages the rod 96 whenv the arm I02 moves upwardly.

It will be apparent that rotation of the shaft |04 will bring about rotation of the crank |06 and alternate raising and lowering of the arm I02 for alternately raising and lowering the ladder like discharge device. the raising and lowering of the discharge device it is oscillated along the length of the discharge board 56. This brings about gradual moving of the residue upthe discharge board, but at such a rate that there is adequate time for the filtrate to drain therefrom back to the tank I4. It will be seen in Figure 1`that the shaft |04 is connected to be driven by the motor 22 so as to rotate simultaneously with the drum I6.

During the period that the filter drum is rotating for continuously renewing the filter coat it is essential that the proper thickness of filter coat be built up in the recoating zone. To insure that the drum will not rotate more rapidly than this coat can be applied, the rate of vrotation of the drum is directly controlled by the thickness of the filter coat in the recoating zone. For effecting this control there is a detector or feeler mechanism which engages the lter cake within the recoating zone and a switch mechanism ycontrolled thereby which controls the driv- Vrthere is a foot or shoe II4 which is carried on a rod I I6 that is pivoted in one of the side plates Y 60 as at II8. The rod IE6 outside the chamber extends upwardly as at I2 so that movement of the part |20 will move the feeler member toward or away from the surface of the filter cake; f

. Due to the fact that Within the recoating zone .there .is a movement of fluidpthrough th`"e filter Simultaneously with :xdetector Y'were to. bearstationarly;againstthe p cake, it would not operate 415o-.detect the;..increased .thickness ofzthef. cake; broughtabout .bys the. de-l r' i positing of;v the?. lter "aid athereon. Accordingly, .1 it' isipreferable -to continuouslysoscillate the 'memberfIM toeandi-.ffromvthe fsurfacerofthe filter --f-.cake Th'sgprovi-des :fora -true feelingV action .of the-membersandjprevents:the; depositedilter` `.iaidffrom"building-.up around the feeler.

oscillationor. the ffeeler.. is acconiplishediby giving: it aspiring-.bias.bythe spring I.I 22.' inra direcrftiontofmove-:thefeeier member toward the cake .@.Inotor shaft vI2 6': offa continuously operating morfftor |28 and isconnected with "afrec-iprocating -:;member I-3ll. .The reciprocating member I 30. car- 1 ries ,1a-.collar I 32 which is adapted for-.engaging 4-the extended Ypart-|2|l ofathe--rodr connected withs:

. vthe-feder and to move the said-'rod Opposite the .-direction Ain...which it. is .biased :by the spring.` I 22. By.v continuously:.driving-the motor :I 28z-the .feeler is continuously!.oscillated.towardfand.awayfrom thecake surface.

.-As. mentionedwbeforefthe rotation of -thedrum u -is` controlledi byrthe eeler. member. vv.Thisl is facjcomplishedebyi a switch...arrangementwhich per- -fmits .energ-izatiorr .of ther drum. drive motor- 22 f only -when .the cake within .the recoating rzonen.

1 -is of the. -properthickness- ...To ,accomplish this function .there .are .a .pairxof ..switches, one of iawhich-ris f indicated .atN LS I in Figure l '7,andthe rfother of which..'consists..ofa pair. of. spaced con- V.tacts.|3|i .oner-of .which .is stationaryand .one of .FW-hich. is carried on the part. I20.of..the feeler sup-v gsporting rod.

Inoperation, the. .cake-V is too. thin. the cone vtacts lI 36I are'. brought. .togetherv `tof energize a. re- ,.lay. |40. ...This relay has,.aholdingcircuit .through r-Wires I44fand |46 and. blade |42 fand.,which cireuit-also-includesthe limit switch LSI. .During Lthettime- `'tl'iat the eelerf'is approaching thecake vwto '1 detect the.' `thickness thereof, the...1imitrswitch LSI is opened bythe col1ar--I38.on.the` rod |30. If the-cake is-.1',oo1thin the contacts |36 .will be -l fclos'edatthis-time so.v that =opening.-of the.` switch .":LSI nwillrmt ioperatevto. Vde'fenergize ...the f aforefmentioned relay. However,if thefcakewis of suf- -fcient thickness @the contacts |36 -will not ...ben-

'closed hand-opening of the switch LS I+ will bring about: de-iener'gization-of the relay. The drum idrive motor is'so connected with theTeIayI-that @ther said motor-willbe-energized fwhen the? relay tisdeeenergized andwill'bede-energizedwhen the vrelay-'is energized.

"mhe .arrangement of'ftheswitch- LSI and'fthe "contacts:V I 36' with fthe drum `,drive fmotor Vis better illustrated in Figure 9 wherein the relay referred "to'zabovel fis'. identiedr :by 1. the reference .numeral -51| l0. The f holding circuit for the said.- relay. is `"'eie'cte'd flthrough .a` blade i425 thereof :.whichxis f-connectedby 'f the fwire-I'M4 with the switch LSI Ytand-:by the wirel |46 -wi'thone of the contacts |36. *LT-heother .of the .'contacts -I 36i isi connectedaby; a 'iWireHIII--at oneside'o a source' 'of' electric; power fl-50, whileanotherff1wire |52 connects 'itheirsame side of the source of electric power with oneside vilftheswitch LSI. The other sideof the^- source .58 endeof .the winding .1. of thea-relay L40 ywhile 1Lathe -rotherzend .of .thersaid winding. is: connected-With the wire.,|-46.

The relaygincludesxthe @blades t56,.a-nd 115.8. .Uponde-energizationof thesrelay a biasingrspring |560 --will `move n it Lto close Av the ,circuits;asso cated with the blades |55 and |58. The'hlaide gISl-iis connected betweenthezpowerilinesrLI and L2 .and z, in series with .the .drum drive :motor 122, while the bladealzisrsimilarly connected '-.between .the -power lines and :in series With 1i the agitator vmotor 1U.

, Since it is ,desirab-le; tozmaintain;the,.slurry;rin the slurry tank 1in: a r state of agitation l,fatnall L times the switchffblade .158,- .is .gbypassedzbyiat'suitableY impedance L62 :whichfzpermits operation-.vof the motor A1|) atifall'atimesizibuttat redncedsspeed exceptwhen Atilelcrladel; I581is closed.

. As previously-.mentioned,pit is?, desiredrolrlyato operate-.the iii-tering device. in:its:.lfter cake-Tren- `ovating' cycle durzing the-,time thatt-therlow rate therethrough is Ireduced -below. a predeter- .minedl :minimum amount z HSoy longgzas fthe vrate of i ui'd flow .throw-fh 1 .the ;yfilter :fisdadequateior lthe purpose for: which theltenisibenemplyed, .it is unnecessary toeifectvany .fooat renovating operations. fHoweverg-rwhenthe, raterof uidfcw through the filter is reducedrto..apredetermined minimum;` this fis. :detected-.by1;rneanseoff the-'idiaphra'gm device identiedrby f the? reference 1 numeral |56. .This .devicenis connectedfby; anconduit |66 with thefydischargevconduit-32 f :of the ipurnp .28.

Associated with a the f; diaphragmfdevice fis 1 a vswitch f |-E8-.which is .adapted-for. being opened when the 4pressure the diaphragm ydevicefis .above a predetermined .amount fia-nd; for bei-ng closed-.when the;v pressure` inrit-he diaphragm- .de-

Vice vfalls .below a1.-Ipredetermined:A amount.

Thus, Vthe-switch 468 cis fopenfwhenfthe-.fiow rate throughthe .-l-ter..is above .-a, predetermined value and is-z closed `.=whenev z-rtit! falls below.; a

`predetermir-ied f-value. ...The -.-sWitch s Ifefisf `connected between' the power lines LIeand. L2...and rin L serieswith the motonwassociated;.withthe filter 0 amount `is to s commence :operation soi ...the dispensen moton Bbwhichleadsftofan addition-,0ff a solid flter aid-material to. theta-nk :62.

Operation In cperation,xlet .itr'beiassurned` thatftheilter -drum'has deposited thereon aii'lterfcakef-ofithe proper thickness and `,that the pump -gin 'operation drawing fluid from: the? inside-@of the 'drum and delivering fitsto-v therA compartment S34. "This zcake, I*which may if consist". ofnfdiatcrnaceous earth or'of a commercialiter-cakezbuilding-irna- 'terialf may be'initially tdepo'sited =on ether-drums vrbytnriereiy rthrowing the cakev formingmaterial tinto Ithevtank elli' whilewtheicirculating jpump is' in'operation The uid foveriiowsfv frein the compartment 3 4- into the; AQta-nk; I El; and thereafter passes-through .thea aperture?! 2` to ,the-'rank1- .I 4, whence itz-isfdrawrr through .the dltendrumr and again passes' through lathe. circulating; pump.

*Thetanks 624s; provided fwith .fiuid frornwthe "compartment 'i3d andeV stands atm-the .same f.level as the fluid therein.

;Let.'.is.be ffurthersassumed...thatsthef-tank B2 'wcon-tainsf substantially l,clean fliquidso...thatfsthere asiatica,

of the drum in the recoating zone. At this time the drum is stationary and the only operation which is taking place is the circulating of fluid through the system' and the continuous oscillation of the feeler member ||4.

If, now, due to the operation of the processing steps taking place in the tank |6,- a residue builds up on the surface of the filtering drum, the flow ratethroughthe pump will gradually reduce due to the clogging of the passages through the iilter cake by the said residue.

When the uid rate through the pump is reduced to a predetermined amount the pressure in the conduit 32 drops and permits the diaphragm device |64 to contract thereby closing the switch |68. When the switch |68 closes, the dispenser motor 84 commences to operate and iilter aid is displaced from the hopper 66 to the tank 62. Y

With lter aid added to the tank 62 and thoroughly Yadmixed with the uid therein by the operation of the agitator propeller 66, a supply of recoating slurry is carried to the recoating Zone between the scraper blades. When this slurry is supplied to the zone the cake on the drum commences to build up therein and this increased thickness of cake is detected by the oscillating member ||4. The cake in the recoating zone will continue to build up and the feeler member will continue to oscillate until the said cake is thick enough that the contacts |36 will fail to close when the feeler member moves in toward the surface of the drum. As explained before the failure of the contacts |36 to close will permit the opening of the switch LSI to de-energize the relay |40 thereby to bring about the closing of the blades |56 and |58 thereof. Closing of the said blades will energize the drum driving motor 22 which will start the drum to rotatingand will increase the speed of the agitator motor 18. The energizaytion of the motor 22 sets the drum in operation whereby the leading scraper blade 54 commences to remove the residue and a portion of the filter cake from the periphery of the drum. Energization of this motor also commences operation of the ladder like discharging device to move the removed residue and filter cake up the inclined drain board 56.

Due to the fact that the drum is moving through the recoating zone the rate at which filter aid is carried into the recoating zone and deposited on the drum is greatly increased. Because of this it is desirable to increase the agitation of the slurry and to this end the motor 1D increases in speed simultaneously with the energization of the motor 22 as explained above.

Rotation of the drum I6 will continue so .long as the cake being built up in the recoating zone is thick enough to prevent the contacts' |36 from closing. However, when the drum ,has rotated apredetermined amount and carried a certain area of clean lter cake from beneath the trailing scraper blade 58, the iiow rate through the pump .will have been increased to the point that the diaphragm operatingvdevice |64 will. again open the switch |68. Openingof the switch |68 will deenergize the dispenser motor 84 and stop the addition of solid lter aid to the tank 62.

Following this, theV drum will continue to rotate so long as the cake thickness prevents the closing of the contacts |36, but within a relatively short time substantially all of the solid material inthe slurry tank will be deposited on the surface of the drumin the recoating zone but without building up a thick enough cake to prevent the contacts |36 from closing. At this time rotation of the drum will halt and will remain halted until additional solid material is fed to the slurry'tank.

The action of the filtering device is accordingly completely automatic, but it will be seen that rotation of the lter drum andthe removal of the residue and cake therefrom is not a continuous process but is only carried out whenever it is necessary to increase the flow rate through the lter to maintain it above a predetermined capacity. The arrangement of this invention is therefore very economical of power and lter aid. 5

Due to the varying conditions of operation or" lters of this type it maybe desirable to remove more or less of the cake during the renovating operation. This may be accomplished by the arrangement shown in Figure 8 wherein the leading scraper blade 54 and the inclined table 56 are arranged to be radially adjustable relative to the drum by means of the screw |16.

Figure 8 also shows the manner in which the lower scraper blade 58 can be adjusted by slidably mounting it on the end of the lower partition 12 of the recoating zone and providing it with an adjusting screw |12 whichis operable to move it toward and away from the surface of the lter drum.

In either case the recoating zone is sealed at its leading and trailing edges by the scraper blades 54 and 58 and at the sides by the sideblades 68 which, as will be seen in Figures 1 and 7, `extend into the cake and preferably somewhat beneath the depth to which the blade 54 scrapes. This gives a sliding contact of the edges of the plates 6|) with the surface of the cake and permits the cake to build up on either side there- 'of to effect a iluid tight seal.

Since the head of the liquid within the entire slurry compartment is greater than that of the uid in the filtering tank |4, any leakage between the recoating zone and the filtering tank will be from the former to the latter. Leakage of this nature might occur when the cake becomes cracked or damaged for any reason and thus does not seal at the blades 54 and 58 or at the end plates 60. However, due to the provision of a greater pressure within the recoating chamber there will be absolutely no contamination of the recoating slurry at any time.

The type of cake which it is desired to build up on the drum is such that it is necessary to maintain a vacuum within the drum to maintain the cake in position. Thus, if the filter is shut down and the vacuum within the drum is completely lost the filter cake will disintegrate and fall to the bottom of the tank I4.

While, by the arrangement of this invention, it is possible to commence operation with a drum completely barren of filter cake and to build a cake thereon automatically, it is preferable that the lter cake be maintained at all times. For accomplishing this the arrangements shown in Figures 10 and 11 may be employed. These arrangements comprise means for physically supporting the lter cake at least during the time that the lter is not in operation. In Figure l0 this is accomplished by a exible screen or other iiexible perforate member |14 which has one end secured as at |16 to the bottom partition of the recoating zone and has its other end connected as at |18 with a lever |86 which is pivoted at y|62 end whieh is adept-ed fer being retired ih a clockwise direction bya I sleridid Si. I

'The perforatemember ,|14 passes around the drum and is preferably normally slightly spaced therefrom. However, upon energization Vof the solenoid SI the lever lllvvillbe rotated and pull the member |14 up againstthesurfaceof the drum. This will physically support the cake and prevent it fromdrepping from'the drum..

It will be apparent that the preferable way to actuate the solenoid Sl would beto interlock it with the drive motor for the pump so that whenever the Vpiilnp- Was shut off the solenoid Si would,bey energized to actuate the holding means for the cake.

A simple electrical circuitfor accomplishing this ,result is connected with the, solenoid Si in Figurel and itcomprises a switc h 84 which, in one positiorn'ene'rgilzes the driveemo'tor 0 for the pump 28, and in its other position energizes thel solenoid Si. Y In Figure 1 1 equivalertresults are obtained by. vmounting s an endless perforated belt, member 86 inv such a manner that it passes aroundthe lterdrum and over a plurality of idlers |88.

The screen or perforate member 186 is driven by. the Idrum and moves therewith Avand continuously offers supporttc the filter cake. Preferably, o ne of `thegidlers is spring urged by a spring |9 in a direction tor maintain a predetermined .tautness in the member.v |86,

Byeither'. of the devices illustrated in Figures 10. and 1.1 the ltergcake can beprevented vfrom disintegratingV and d lQpp'ing from the drum when the vacuum inthe said drum is lost.

Preferably, in combination with the holding devices for the iilterl cakeuthe. conduit 25 in cludes a check valve. 192 opehingfrom the drum toward the pump 28 and operable to prevent a back rush of fluid from thepump when the same is halted. The checkvalvein itself will prevent disintegration ofthe Vfilter cake, for a matter of some minutes, and in any caselwill prevent. back washing of the cake which in many cases would be destructive thereto.

Modifications of Figures 1-2 and 13 Some types of lter aid whenlacted on byl a scraping blade such as the blade 54 have a itendency to become glazed over.. This is due to the factthat the 4,scraper blade probably `crushes some of the particles of filter aid and forces them. into the, pores Qi the Cake as the drum rotates. Due to this .glazing overaction .of the cake Ain vconnection with ertaintypes of lter aid the flow rate throughthe cake may be materially reduced after aperiod `of operation.

For overcoming this. drawback in connection with those types of lter: aid which react in this manner, the constructions shown in Figures 12 and lmay be employed.

InFigure 12 the scraper blade is indicated at 200 and comprises a thin vflexible blade which lies over aiportenof thesurface of the drum 46. The blade 2e!)y nts closely againstthedruni and is thus operableto remove substantially all of thecake therefrom.`

Inasmuch as theblade 291i isfdu'ite .thin and flexible it is preferable that it be backed up by aresilient member such as the rubber. bl'ock 202 which exerts pressure lover the surface of the blade andfhclds it against the suV ,o'f the drum.r metal clip.. 2'04 or other Asuitable means can be; employed fr exerting ya 'pressure on the bIo'ck'202.

. and is y effective toV .prevent the vacuum within the' drum fromactin'g over'` the shield part@ As'v `Inasiru-cl'1'as "it is asfpdssibie er thev cake from the' drurrixas it. passes beneathvthe scraper lblade 200 it may be preferable to shield alltio'n of, thev drumy immediatelybeneaththe said blade vas by means of themask206. The said mask covers the drum beneath the made 2cm and also extends' forwardly.v and rearwardly from the said `bladge moet filter aid materialsdepehd upon the vacuum within the ,drum to retain them in cake form thereon, it will be apparentthat alinasking of a portion ofy the dr'uni .as shown in Figure 12 will permit the cake tc lcosen `thereon and givevit a tendency to disintegrate. 'Because of this` losen'ingcf thecake the scraper blade Zfilvis effective for removing substantially all thereof.

The covering vmember 48 Vfor the drum is,.. as npie'ntinedv before, preferably a wire screen. Becausey of the .nature .of the wire screen andthe perforate nature of the. drum vthere will be little hollows and depressions extending over the surface of the drumfrc'm which the scraper blade 260 cannet effectively remove the lterwcake, For this reason *thev shield v2416 is' extended behind the blade 2132 and thus r,masks'oi the portion cf the 'dr-um over which t he sflurry ofrecoatingmat'erialis passing as atf208. Since this slurry is beingdire'cted toward the .surface of the drum as a Jfairly high' velocity jet, it will dislodge the remnants of vthe lil'tfe'r cake' from the drum which has passed beneath the' knifeblade, pick up the` removedparticles 'and direct theminto the slurry stream. `'I helcake which is formed on the, drum .in the recb'ating chamberis thus substantially new throughout 'its entire depth. v

It will .he uhdersto'od Tthat th'1e actuar thickness f viilter cake to b'e built up on the drum in the recoatir'ig cha'mlznjer.will b fey dependent upon the. nature of the vfiltering 'operation being carred out andthe degree of purity which is desiredin the ltrate.i.

The vshield ZDBniaybge arranged within th'e dru'mas .shown in Figure 13 Vwherein it will be se'enlthat thevsaidwshield comprises ,a hub part 2 'I0wh'i`ch is's'ecuredto fa sleeve Zl2 that extends tlirllg'h the Hub 2H 0f the head `0f the drum atthat end. l

. The 'sleeve 2fl2is secured as by the screws 216 tdlthe frame [2,0 tor someother suitable station.- ary .part andfactsasfa journal "for the drum at its outer surface andz'forithe shaft 4i) at its inner Si'irfae.A suitable sealing means suw as the resilient rines indicated. at 2113V prevent leakage between vtl'iefsleeve' member and the drum or between thesleeve' member :and 'the shaft.k

In ,cdnhection with Figures k12 and 13 it is to be observedthat the blade ZBO is shown considerably Atl'icke'r, thaI'r-it actually isfor the sake of clarityand 'beth the .blade Zi) and the mask V201i arefs'hlo'wnasspaning considerably 'more of the periphery or the' drum than actually occurs.

.In practice, theexiblefblade 2 00 would probably be 'effective if itcove'rd 'a half an inch of the; Vperiphery of a drum 'that was, say, 4 to 5 inches 'in diameter. A'Ih'ejshield or mask 2,06 in that case wuld probablyjeiitend from a quarter to a half inch ahead o`f the leading edgeofgthe blade v200 and from aguarter to a halfjin'c'h to the rear thereof.` It iwill be apparent from the dimensionalde'scripti'ofnjabove thatthe blade and shield, maskI out only a very minor portion of It win be understood that this ih'vehue'n is resiente remue as ril-eeh;

susceptible to modifica-in in order to adapt it to different usages and conditions and, accordingly, it is desired to comprehend such modifications within this invention as may fall within the scope of the appended claims. Y 4

We claim: Y

1. In combination; a first tank having liquid therein to be filtered, a second tank hydraulically connected with said first tank and thus having the same liquid level, a rotary drum in said second tank normally completely submerged in the liquid therein and being foraminous, means for drawing a lvacuum in said drum to induce fluid flow therein from said second tank, spaced scraper blades bearing on the peripheryvofsaid drum, a chamber between said blades opening against the surface of said drum to supply a cake forming slurry thereto, means for supplying a slurry forming material to Ysaid chamber, and means for maintaining a pressure .in said chamber above that of the liquid in said front tank comprising; a compartment in said first tank having a wall above the liquid level in the said tank, a conduit connecting said compartment with said drum to receive iiltered fluid therefrom, said fiuid overflowing intothe said first tank, and a hydraulic connection from said compartment to said chamber. Y

2. In combination; a pair of tanks for liquid to be filtered and hydraulically connected at their bottoms, a rotary drum in one of said tanks and normally completely submerged in the liquid therein, a compartment in the other of said tanks having its walls above the liquid .level in said tank, a pump connected to draw fluid from within said drum and to supply it to said compartment whereupon the fiuid overflows into the tank around said compartment, spaced scraper blades bearing on the periphery of rvsaid drum, end plates connecting said blades and forming therewith a chamber opening against the surface of said drum for supplying a cake forming slurry thereto, means for supplying dry cake forming material to said chamber, and means for supplying liquid to said chamber and for maintaining the pressure thereon above that of the liquid in said tanks comprising a hydraulic connection between said chamber and said compartment.

3. In combination; first and second tanks hydr-aulically connected at their bottoms, means in said iirst tank forming a compartment having a liquid level above the normal level in said tanks, a rotary perforate drum completely submerged in said second tank, a pump having itsI inlet connected with the inside of said drum and its outlet connected with said compartment, a first scraper bl-ade bearing on said drum to remove residue and a portion of the filtered cake therefrom as it rotates, a chamber opening against the surface of said drum behind said blade to supply a recoating slurry to the drum, a slurry tank' hydraulically connected with said chamber and extending to above the liquid level of s-aid first and second tanks, said chamber ,and

slurry tank being isolated from the liquid in said i4 tanks, a rotary periorate drum completely sub-f merged in said second tank, a pump having its inlet connected with the inside of said drum and its outlet connected with said compartment, a scraper blade bearing on said drum to remove residue and a portion of the filtered cake therefrom as it rotates, a chamber of which said blade forms one wall opening against the surface of said drum behind said blade to supply a recoating slurry to the drum, a slurry tank hydraulically connected with said chamber and both said slurry tank and chamber being hydraulically isolated from the liquid in said second tank, a conduit connecting said slurry tank with said compartment to supply fluid to the slurry tank. means for supplying solid filter aid to said Vslurry tank to form said slurry with said fluid, and means in said slurry tank for causing the said slurry to circulate therein and in said chamber to hold the solids in the slurry in suspension.

5. In combination; first and second tanks hydraulically connected at their bottoms, means in said rst tank forming a compartment having a liquid level above the normal level in said tanks, a rotary perforate drum in said second tank, lying wholly below the said normal level a pump having its inlet connected with the inside of said drum and its outlet connected with said compartment, a scraper blade bearing on said drum to remove residue and a portion `of the lter cake therefrom as it rotates, a chamber of which said blade forms one wall opening against the surface of said drum behind said blade to supply a recoating slurry to the drum, a slurry tank hydraulically connected with said chamber, a conduit connecting said slurry tank with said compartment to supply fluid thereto, means for supplying solid iilter aid to said slurry tank to form said slurry with said fluid, and means in said slurry tank for causing said slurry to circulate in said slurry tank and chamber to hold the solids in the slurry in suspension, said chamber including means for causing the circulatory slurry flow therein to take place over the surface of said drum thereby preventing an over accumulation of filter aid at the drum.

6. In a filter, a rota-table filter drum, means energizable for driving said drum, a scraper blade bearing on the cake on said drum to remove a portion thereof as said drum rotates, a chamber immediately behind said blade to supply a, slurry of recoating material to the surface of said drum to replenish the cake removed by said scraper, a feeler in said chamber adapted to engage the surface of the cake on the drum therein, and means controlled by said feeler operable to prevent energization of said drum driving means when said cake is less than a predetermined thickness and to bring about energization of said driving means lwhen said cake is equal to or greater than said predetermined thickness.

'7. In a filter, a rotatable cake supporting lter drum, means energizable for driving said drum, scraper means bearing on said cake to remove a portion thereof as said drum is driven, a chamber immediately behind said blade to supply a slurry of recoating material to said drum to replenish Ithe cake removed by said scraper, a feeler in said chamber adapted to engage the surface of the cake on the drum therein, means continuously oscillating said feeler toward and away from the surface of the cake on said drum, and means operated by said feeler and responsive to thethickness of the cake on the drum immediately following said blade and a slurry tank hydraulically connected therewith, a dispenser to supply dry cake forming material to said tank, means to supply fluid to said tank to form a slurry therein with said dry material, a feeler in said chamber resting on the surface of the cake on the drum therein to detect the thickness of the cake, control means for said drive motor connected with said feeler and operated thereby to energize said drive motor when said cake reaches a predetermined thickness, means responsive to a predetermined minimum discharge rate of said pump for actuating said dispenser, and to a discharge rate of said pump greater than said predetermined rate for halting the action of said dispenser, and agitator means in said tank for maintaining the dry material dispensed by said dispenser in suspension with said fluid.

17. In a drum type vacuum filter; having a rotatable perforated drum mounted on a horizontal axis and adapted for supporting a lter cake when a vacuum is drawn on said drum, a pump connected to draw a vacuum on said drum, a perforated flexible member of substantially the same width as the drum passing around the lower part of said drum and normally spaced therefrom, and means operative when said pump is running for maintaining said member spaced from said drum, said means being operable when said pump is halted for automatically moving said flexible member toward said drum to engage and support the cake thereon.

18. The method of operating a drum type Vacuum filter wherein the said drum is rotatably suspended submerged in the fluid to be filtered and a vacuum is drawn thereon to induce fluid flow through the drum comprising; sealing off a part of the periphery of the drum from the uid in which the drum is submerged, presenting a part of the ltered uid drawn through the drum to the sealed o part of the outside surface of the drum, adding lter aid to the uid so presented to build up a cake on the said part of the drum, rotating the drum when the cake on the said part reaches a predetermined thickness thereby to carry another portion of the drum to the re-presented fluid, and halting the addition of filter aid to the re-presented fluid whenever the flow rate through the drum reaches a predetermined value.

19. The method of operating a drum type vacuum lter wherein the drum is rotatably supported submerged in the uid to be filtered and a vacuum is drawn on the drum to induce fluid ow therethrough comprising; sealing o a part of the periphery of the drum, presenting a slurry of cake forming material to the said part of said drum, rotating the drum. when the cake built up on the said part thereof exceeds a predetertermined thickness, increasing the concentration of the slurry when the flow rate through said drum falls below a predetermined amount, and scraping off at least a part of the cake from the drum immediately ahead of the area to which said slurry is presented.

20. The method of operating a drum type lter wherein a cake supporting drum is submerged in the fluid to be filtered and a vacuum is drawn on the interior of the drum to induce fluid flow through the cake thereon comprising; sealing oi a portion of the peripheral extent of the drum from the fluid to be ltered by spaced scraper elements of which the leading is closer to the drum surface than the trailing and supplying liquid to the sealed off portion, adding cake forming material to the said liquid whenever the flow rate through the drum is below a predetermined amount, rotating the drum when the cake formed on the sealed off portion exceeds a predetermined thickness, and halting the addition of material to the said liquid when the flow rate through the drum again reaches the said predetermined amount, whereby said filter is maintained in continuous operation.

21. The method of operating a drum type lter wherein a cake supporting drum is submerged in the fluid to be filtered and a vacuum is drawn on the interior of the drum to induce fluid flow through the cake thereon comprising; rotating the drum, scraping the drum at spaced points therearound, adding new cake to the drum between said points by applying a slurry of nlter aid thereto, rotating the drum when the new cake built up thereon is equal to or greater than a predetermined thickness, and varying the concentration of the cake forming slurry inversely to the changes in the rate of fluid ow through said cake.

22. The method of filtering comprising; completely submerging a ltering member in fluid to be filtered, drawing a vacuum on one side of the member to induce iiuid ow therein, sealing off a part of the outer surface of the other side of the member, supplying a recoating slurry to the member in the sealed oi area whereby the vacuum on the other side ofthe member will draw fluid from the slurry and cause the solid material in the slurry to build a cake on the surface of the member, moving the member and the sealed olf part relatively whenever the cake formed in the sealed off area reaches a predetermined thickness, adding dry cake forming material to the slurry when the flow rate through said member falls below a predetermined amount and halting the addition of solids to the slurry whenever the ow rate through said member exceeds said predetermined amount, and maintaining a head on said slurry above that of the fluid to be filtered thereby to prevent contamination of said slurry by the leak- REFERENCES CITED The following references are of record in the file of this patent:

UNITED STATES PATENTS Number Name Date 45,149 Foote Nov. 22, 1864 206,107 Hatch July 16, 1878 898,212 Gaara, et al Sept. 8, 1908 1,103,725 Woodman July 14, 1914 1,227,983 Vallez May 29, 1917 1,515,130 Morrison Nov. 11, 1924 1,579,171 yZoul Mar. 30, 1926 1,796,491 Sweetland Mar. 17, 1931 1,848,478 Haug Mar. 8, 1932 1,906,767 Roberts May 2, 1933 2,102,780 Bielfeldt Dec. 21, 1937 2,092,111 Dons et al. Sept. 7, 1937 2,473,270 Adams June 14, 1949 FOREIGN PATENTS Number Country Date 339,636 Great Britain Dec. 8, 1930 805,309 France Nov. 17, 1936 

